Composition and methods for injection of sealants into air conditioning and refrigeration systems

ABSTRACT

The use of sealants based on organosilanes for refrigeration and air conditioning systems is made possible by control of the rate of introduction and viscosity of the sealant mixture within certain ranges. An appropriate choice of organosilane sealant is made to allow effective sealing of small pinhole size leaks in the air conditioning or refrigeration system. The organosilane is then combined with a miscible lubricant at particular ratios to provide the proper mixture viscosity for injection into the refrigerant system to prevent bearing seizure. Specific orifice sizes are selected for an apparatus to ensure that the composition is injected at the flow rates required to prevent liquid slugging and subsequent compressor shutdown or failure. In addition, effective introduction of the mixture requires certain procedures be performed. Injection procedures are also described that prevent temporary or catastrophic equipment shutdown.

FIELD OF THE INVENTION

The general field of the invention is the injection of sealant intorefrigeration and air conditioning systems by means of suitableselection of sealant, mixtures, equipment and procedures to seal smallleaks that develop in the system.

BACKGROUND OF THE INVENTION

Organosilanes have been marketed successfully as automotive airconditioning (A/C) system sealants for several years. Their use istargeted at small pinhole leaks that develop over time, allowing escapeof refrigerant. Leaks lead to loss of efficiency for the a/c system aswell as undesirable release of refrigerant gas to the environment. Theapplication of these sealants to hermetically sealed systems used innon-automotive a/c systems and in refrigeration systems has been lesswidespread. In these applications, sealant injection often leads tocompressor shutdown due to bearing seizure. At least one sealantmanufacturer recommends the use of a “hard-start kit” apparently toovercome this issue.

It is desirable to develop alternative products and methods for theintroduction of sealant into air conditioning and refrigeration systems.

SUMMARY OF THE INVENTION

In a first aspect the invention provides a method for injecting sealantinto an air conditioning or refrigeration system having a compressor, ahigh pressure side (“high side”), and a low pressure side (“low-side”).The method includes injecting the sealant in a quantity to providesufficient lubrication to maintain proper operation of the compressorwhen the sealant is fully distributed in the system, and injecting thesealant so as to maintain proper operation of the compressor before thesealant is fully distributed in the system.

The sealant may be injected at the high side of the system so as tomaintain proper operation of the compressor before the sealant is fullydistributed by distributing the sealant starting at the high side. Theinjected sealant may be injected at a rate of less than 6% per minute oflubricant within the system.

The sealant may be injected at a controlled rate so as to maintainproper operation of the compressor before the sealant is fullydistributed in the system.

The sealant may be injected into a non-operating system under vacuum,and other system contents, including refrigerant, are later injectedinto the system causing distribution of the previously injected sealant.Approximately 60% of total system refrigerant may be injected after thesealant.

The sealant may be injected as a part of a fluid mixture, and themixture further comprises one or more of lubricant, drying agent,corrosion/rust inhibitor, antiwear agent, fluorescent or phosphorescentdye.

The sealant may be an organosilane. The organosilane may be a monomercapable of forming a solid polymer with itself or other chosenorganosilanes in the presence of moisture, and is stable in the absenceof moisture, and does not substantially interfere with the normaloperation of other contents of the system in selected quantities.

The sealant may be part of a fluid mixture further comprising alubricant. The lubricant may be an oil, the compressor may have a sumpcontaining oil, and the minimum viscosity of the injected fluid mixturemay be η_(inj) as determined by:exp(x _(inj) .lnη _(inj) +x _(sump) .lnη _(sump) +C)≧Fr.η _(sump)

-   -   where,    -   ln is the natural logarithm and exp is the exponential,    -   η_(inj), is mole fraction of injected material in final sump        mixture,    -   x_(sump) is mole fraction of original sump oil in final sump        mixture,    -   η_(inj), η_(sump) are viscosities of the injected material and        original sump oil respectively, and    -   Fr is a desired fraction of original sump oil viscosity to be        maintained.

Fr may be equal to approximately 0.9 or more.

The viscosity of the mixture may be not less than 7 CST @ 40° C.

In a second aspect the invention provides a method of introducingsealant into an air conditioning or refrigeration system having acompressor and evaporator. The method includes connecting a vesselcontaining a sealant mixture comprising an organosilane between thecompressor and the evaporator, and while the system is running, allowingthe sealant mixture to enter the system at a rate to prevent liquidslugging and to maintain sufficient concentrations of lubricant forproper operation of the compressor during the injection process,allowing the sealant to enter the system in an amount to maintainsufficient compressor lubricant viscosity for continued proper operationof the compressor, and allowing the sealant to enter in an amount thatwill allow continued proper operation of the air conditioning orrefrigeration system.

In either aspect the sealant may be one or more of an organosilane and apolymeric latex consisting of one or more of a vinyl acetate,methacrylate, nitrile, epoxide and styrene polymer. The mixture may alsoinclude one or more of an accelerant and a catalyst.

The sealant mixture may be allowed to enter the system by pressurizingthe sealant mixture sufficiently above system low side operatingpressure to cause the sealant mixture to enter the system from thevessel when the system is running. Pressurizing the sealant mixture mayinclude using the system pressure of the system in a non-running stateto pressurize the sealant mixture in the vessel.

The method may also include allowing the sealant mixture to cool to nearambient temperature after the vessel is pressurized and while the vesselis fluidly connected to the system in the non-running state. The methodmay also include fluidly disconnecting the pressurized vessel from thesystem after cooling, running the system until low side pressure drops,and fluidly connecting the vessel to the low side of the system andallowing the sealant to enter the system as provided above.

In a third aspect the invention provides a method of introducing sealantinto an air conditioning or refrigeration system having a compressor andan evaporator. The method includes turning off the system; allowingsystem pressure to equalize; connecting a vessel containing a sealantmixture comprising an organosilane between the compressor and theevaporator, and while the system is running, allowing the sealantmixture to enter the system at a rate to prevent liquid slugging and tomaintain sufficient concentrations of lubricant for proper operation ofthe compressor. The organosilane is a monomer capable of forming a solidpolymer with itself or other chosen organosilanes in the presence ofmoisture, and is stable in the absence of moisture in the system, anddoes not substantially interfere with the normal operation of contentsof the system in selected quantities.

The step of connecting the vessel may include providing fluid connectionbetween the vessel and the system, and the method may further includeallowing sufficient time for the sealant mixture to achieve ambienttemperature before running the system after fluid connection.

The method may further include turning off the system when a selectedamount of sealant mixture has entered the system for a period of time toallow system pressure to equalize, and repeatedly allowing the sealantmixture to enter the system as specified above and turning off thesystem to allow pressure to equalize as set out above, until a totalselected amount of sealant has entered the system. The method mayinclude equilibrating the system after injecting the approximately 60%of the refrigerant then turning on the system and adding remainingrefrigerant.

The sealant mixture may have a viscosity above 7 cst. when measured at40° C. The flow rate of injection may be 6 cc/sec or less.

The viscosity for a particular lubricant/sealant mixture may be η_(inj)or greater where η_(inj) is determined by:exp(x _(inj) .lnη _(inj) +x _(sump) .lnη _(sump) +C)≧Fr.η _(sump)

-   -   where,    -   ln is the natural logarithm and exp is the exponential,    -   x_(inj) is mole fraction of injected material in final sump        mixture,    -   x_(sump) is mole fraction of original sump oil in final sump        mixture,    -   η_(inj), η_(sump) are viscosities of the injected mixture and        original sump oil respectively, and    -   Fr is a desired fraction of original sump oil viscosity to be        maintained.

Fr may be equal to 0.9 or more. Where the calculated viscosity may beless than 7 cst., then the minimum viscosity may be set at 7 cst.

The step of allowing the sealant to enter the system may further ncludeallowing the sealant to enter through an orifice having an openingwithin a range of from 0.020-0.06 inches diameter.

The step of connecting the vessel to the system may include connecting ahose assembly between the vessel and a low pressure side service port ofthe system. The hose assembly may include a first fitting for connectionto the vessel and a second fitting for connection to the port.

The step of providing fluid connection between the vessel and thesystem, and the step of allowing sealant mixture to enter the system,may include opening a valve in the second fitting.

The vessel may be a sealed canister, and the step of providing a fluidconnection between the canister and the system may include tapping thecanister before opening the valve in the second fitting.

The second fitting may be a can-tapper. The method may also includesubstantially evacuating the hose assembly prior to connection to thesystem.

In a fourth aspect the invention provides a device for introducingsealant into a hermetically sealed air conditioning or refrigerationsystem. The device includes a sealed vessel including an organosilanemixture of an organosilane and a miscible material, the mixture having aviscosity above 7 cst. when measured at 40° C. In this aspect theorganosilane is a monomer or oligomer capable of forming a solid polymerwith itself or other chosen organosilanes in the presence of moisture,and is stable in the absence of moisture in the system, and does notsubstantially interference with the normal operation of contents of thesystem in selected quantities.

The device may include a metering device for fluid connection with thesealed vessel, and for controlling fluid flow from the sealed vessel.The metering device may be an orifice having an opening within a rangeof from 0.020-0.06 inches.

The device may further include a fitting for sealed fluid connection toa low side port of the system, and the fluid flowing through themetering device also flows through the fitting. The device may alsoinclude a hose assembly with a first fitting for sealed fluid connectionto a low side port of the system, and a sealed fluid connection to thesealed vessel.

The device may also include a metering device for controlling fluid flowfrom the sealed vessel through the hose assembly.

The fluid connection to the sealed vessel may be a second fitting. Thesecond fitting may include a manually operable valve for providing fluidconnection between the hose assembly and the sealed vessel. The secondfitting may include a can-tapper for opening the sealed vessel.

The device may include a filter is placed between the fitting connectingto the system and the orifice. The orifice may have a diameter of 0.06inches or less. The sealed vessel may be a sealed canister.

The organosilane or components of the sealant mixture may includecomponents that can be represented as (R₁)(R₂)Si(R₃)(R₄)

-   -   where,    -   R₁=is an alkyl radical of 1-4 carbon atoms or vinyl or —OH    -   R₂ is R₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂,    -   R₃ is R₁ or —OR₁ or —NH(R₁) or —N(R1)₂ or —R₁NHR₁NH₂, and    -   R₄ is R₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂

A component of the sealant mixture may include components that can berepresented as(R₅)(R₆)(R₇)Si—O—Si(R₅)(R₆)(R₇)

-   -   R₅, R₆ or R₇ are each any one of R₁,R₂,R₃ or R₄ where,    -   R₁=is an alkyl radical of 1-4 carbon atoms or vinyl or —OH,    -   R₂ is R₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂,    -   R₃ is R₁ or —OR₁ or —NH(R₁) or —N(R1)₂ or —R₁NHR₁NH₂, and    -   R₄ is R₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂

The sealant mixture may also include a lubricant miscible with theorganosilane and refrigerant for use in the system. The miscible mixturemay include a lubricant selected from one or more of a polyol ester,polyalkylene glycol, mineral oil, polyalphaolefin and alkylbenzene. Themiscible mixture may include a lubricant further comprising additives toenhance and refresh the performance of lubricant in the compressor.

The preferred embodiment of these and other aspects of the inventionwill be described later herein.

BRIEF DESCRIPTION OF THE DRAWINGS

For a better understanding of the present invention and to show moreclearly how it may be carried into effect, reference will now be made,by way of example, to the accompanying drawings which show the preferredembodiment of the present invention and in which:

FIG. 1 is a graphic representation of a sealant injection assembly inaccordance with a preferred embodiment of the present invention in usewith an air conditioning or refrigeration system 1.

FIG. 2 is a partially exploded perspective view of the assembly of FIG.1.

FIG. 3 is an end view of a fitting and orifice used in the assembly ofFIG. 2.

FIG. 4 is a cutaway view of a typical single cylinder hermeticcompressor.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT

Referring to FIG. 1, a typical hermetically sealed air conditioning orrefrigeration system 1 has an evaporator 3, compressor 5, condenser 7and expansion device 9. The system 1 has a “low side” 10 consisting ofthe part of the system 1 between the expansion device 9 (for example, anorifice 9) and the suction line to the compressor 5. The compressor 5draws in low pressure, low temperature refrigerant in a gaseous statefrom the “low side” 10. The compressor 5 compresses the gaseousrefrigerant to a high pressure, high temperature gaseous state thatflows to the condenser 7. The refrigerant passes through the condenser 7and is cooled to a liquid state. The liquid refrigerant passes throughthe expansion valve 9, which causes the refrigerant to expand to a lowpressure, low pressure temperature gas. The evaporator 3 absorbs heatfrom outside the system 1, and relatively low temperature, low pressuregas is reintroduced to the compressor 5.

For the test environment, the low side pressure is 77 psig at thecompressor 5, and pressure on the high pressure side of the compressor(the discharge 11) is 256 psig. The temperature at the evaporator 3 is45° F. and at the condenser 126° F. The ambient temperature is 90° F.The temperature of the gas between the valve 9 and evaporator 3 is 55°F. The temperature at the compressor 5 discharge 11 is 171° F. Theorifice 9 in the test environment had a diameter of 0.059 inches. Thegas flow rate in the low side between the evaporator 3 and thecompressor 5 is 1596 ft/min. The diameter of pipe in the low side isnominal ¾ inch, while the inside diameter of pipe at the discharge is3/8 inches. This is for a single phase 2 ton compressor 5.

These are typical characteristics for an air conditioning system 1 orthe environment about an air conditioning system 1. For larger andsmaller systems 1, the particular specifications may change. This adesign choice. The particular parameters under which sealant isintroduced into the system may vary accordingly.

In order to seal small leaks in the system 1 it is desirable tointroduce organosilanes or other sealants into the system 1.Organosilanes cure when in the presence of moisture, such as would occurat the situs of a leak.

The use of organosilanes in non-hermetically sealed air conditioning orrefrigeration systems 1 is previously known, see for example, U.S. Pat.No. 4,237,172 issued 2 Dec. 1980 to Packo et al under title SealingLeaks by Polymerization of Volatilized Aminosilane Monomers; U.S. Pat.No. 4,304,805 issued 8 Dec. 1981 to Packo et al under title SealingLeaks by Polymerization of Volatilized Aminosilane Monomers; U.S. Pat.No. 4,331,722 issued 25 May 1982 to Packo et al under title SealingLeaks by Polymerization of Volatilized Organosilane Monomers; and U.S.Pat. No. 5,417,873 issued 23 May 1995 to Packo under title SealantContaining Partially Hydrolized Tetraalkoxy Silane, for Air Conditioningand Refrigeration Circuits that describe mixtures for this purpose. Aspreviously mentioned, the simple injection of an organosilane or mixtureof organosilanes into a hermetically sealed system 1 will typicallycause compressor 5 failure.

Referring to FIG. 2, an injection assembly 12 has a vessel 15 containingan organosilane mixture. In the preferred embodiment the vessel 15 is acanister 15. The mixture is selected for miscibility with the contentsof the system 1. It is to be recognized that, in addition torefrigerant, the system 1 contains a miscible lubricant for lubricationof the compressor 5. The system 1 may also have other contents, such asa fluorescent dye for leak detection. It may also contain a chemicaldryer to remove moisture from the system 1.

The inventors have recognized that, in addition to liquid slugging, theintroduction of greater concentrations of organosilanes removelubricants from the compressor 5, resulting in compressor 5 failure. Theorganosilane should be introduced in sufficiently low concentrations andbe miscible with the system 1 lubricant to avoid liquid slugging and tomaintain sufficient lubricant for proper operation of the compressor 5.The organosilane is introduced from vessel 15 to a low side port 17between the evaporator 3 and compressor 5.

The organosilane is introduced at a rate that allows the concentrationof the organosilane to be diluted sufficiently by the other system 1contents to prevent liquid slugging and to maintain sufficientconcentration of lubricant for proper operation of the compressor 5.

Referring to FIG. 4, controlled injection of the organosilane combinedwith the miscible lubricant is critical when injected at the low sideport 17 because of the close proximity between the low-side chargingport 17 and compressor 5. After the organosilane/miscible lubricantmixture enters the compressor 5 along with cool refrigerant vapor it hasto first pass by outboard shaft bearing 18. This aids in replacing oilto the outboard bearing which may have been stripped by passingrefrigerant. The mixture continues on flow path 19 a rushing over motorwindings (stator 19 b, rotor 19 c) removing heat from the electricmotor. The flow of refrigerant vapor/mixture is then drawn over oilreservoir (sump) 19 d into compressor pump 19 e where it is compressedinto a hot vapor and discharged. During this flow path the importance ofmaintaining a suitable viscosity is important for a continued oilbarrier between metal internals.

Many refrigeration and air conditioning systems use semi-hermetic oropen seal (external drive) compressors and the type of compressor may bereciprocating (piston-cylinder), rotary, scroll, screw or centrifugal.While compressor geometry is critical to the hermetic systems asexplained above, general engineering considerations also require controlof flow rate, quantity and viscosity of the injected material for theother drives to ensure continued good operation and acceptablecompressor life.

The organosilane can be introduced by many different methods. Forexample, it can be injected at a very slow rate while the compressor 5is running continuously. This requires fine control over the injectionrate. In order to allow increased rate of introduction, theorganosilanes (or a portion thereof) can be injected into a runningsystem 1, followed by a period of time during which the system 1 isstopped. The initial use of a running system 1 allows the organosilaneto be distributed through the system 1. Stopping the system 1 allows thedistributed organosilanes to further mix with the system 1 contents,without forcing areas of high organosilane concentration to flow throughthe compressor 5 repeatedly. This process can be repeated until all ofthe organosilane is introduced. Although this may allow for greaterrates of introduction, the process would still be slow, and fine controlis still required.

An alternative method of introducing the organosilane is to form anorganosilane mixture by pre-diluting the organosilane in a materialmiscible with the system 1 contents and with the organosilane. Thismixture is then introduced into the system 1 using one of the methodsdiscussed above.

In the preferred embodiment, the organosilane is mixed with a lubricantto form the organosilane mixture. This has an additional benefit ofmaintaining lubricant in close proximity to the organosilane at alltimes. For increased flow control the viscosity of the organosilanemixture can be maintained within a selected range. Organosilane on itsown has a very low viscosity (for example <1 cst. at 40° C.). This inpart results in difficulty in controlling the flow of organosilane.

An additional method of injection would include the use of a fluidinjector that can inject the mixture into the working low side system ofthe unit in small increments, an example include a Revolver™ sold byCliplight Manufacturing Company of Toronto, Canada. The Cliplight deviceallows for approximately 0.04 of an ounce to be measured in at any onetime. Additional amounts of the mixture depending on the system sizecould be accurately added. This would be an acceptable method ofinjection allowing only small amounts of the mixture into the suctiongas path and thus preventing possible liquid slugging to the compressor5.

Also, there are other modifications that could be made to an injectiondevice. For example, a filter could be added to the hose apparatus 16 tofilter out any particles injected from the system 1 when charging thecanister 15.

Further details of the preferred embodiment will be described.

Referring to the FIGS., the use of sealants based on organosilanes forrefrigeration and air conditioning systems 1 is made possible by controlof the rate of introduction and viscosity of the sealant mixture withincertain ranges. An appropriate choice of organosilane sealant is made toallow effective sealing of small pinhole size leaks in the airconditioning or refrigeration system 1.

Preferably, the organosilane is chosen with several criteria in mind.The organosilane is miscible in the lubricant fluid; it is typically amonomer, but may contain oligomers, capable of forming a solid polymerwith itself or other chosen organosilanes in the presence of moistureunder the conditions of the particular application. The reaction rate ofthe organosilane or mixture of organosilanes is sufficient to form aneffective seal at the situs of the leak. The polymeric seal is chosen tobe sufficiently strong to maintain an effective barrier to preventfurther leakage of refrigerant from the system 1. Also, theorganosilanes are chosen to be stable in the absence of moisture, benon-corrosive and otherwise inactive to the components of system 1 andbe generally environmentally acceptable. Further, the nature andinjected quantity of the organosilanes is chosen, to the extent that itwould interefere with the refrigerant and/or lubricant, so that suchinterference remains consistent with the normal operation of therefrigerant fluid e.g. vaporization and liquefaction characteristics.

The organosilane is combined with a miscible lubricant at particularratios to provide the proper mixture viscosity for injection to therefrigerant system 1 to prevent bearing seizure. Specific orifice 20(see FIG. 3) sizes are selected for an apparatus to ensure that themixture is injected at flow rates required to prevent liquid sluggingand subsequent compressor 5 shutdown or failure. In addition, certainprocedures are performed for effective introduction of the mixture.Injection procedures are also described that reduce risk of temporary orcatastrophic equipment shutdown. These include allowing the sealantmixture to cool to ambient temperatures before injection. Coolingpermits better control over the flow rate of the organosilane componentof the mixture.

Preferred components and compositions for the organosilane include thosedescribed in U.S. Pat. No. 4,237,172 issued 2 Dec. 1980 to Packo et alunder title Sealing Leaks by Polmerization of Volatilized AminosilaneMonomers; U.S. Pat. No. 4,304,805 issued 8 Dec. 1981 to Packo et alunder title Sealing Leaks by Polmerization of Volatilized AminosilaneMonomers; U.S. Pat. No. 4,331,722 issued 25 May 1982 to Packo et alunder title Sealing Leaks by Polymerization of Volatilized OrganosilaneMonomers; and U.S. Pat. No. 5,417,873 issued 23 May 1995 to Packo undertitle Sealant Containing Partially Hydrolized Tetraalkoxy Silane, forAir Conditioning and Refrigeration Circuits.

Particular compositions for the organosilane are dependent on theselected criteria from those set out above. However the general natureof the organosilane can be represented as (R₁)(R₂)Si(R₃)(R₄) where thepreferred nature of the radicals is that

-   R₁ is an alkyl radical of 1-4 carbon atoms or vinyl or —OH-   R₂ is R₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂-   R₃ is R₁ or —OR₁ or —NH(R₁) or —N(R1)₂ or —R₁NHR₁NH₂-   R₄ is R₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂

Other components which can be included are oligomers of the monomericsilanes described. One such example are the siloxanes:(R₅)(R₆)(R₇)Si—O—Si(R₅)(R₆)(R₇)

-   -   Where R₅, R₆ or R₇ may be R₁,R₂,R₃ or R₄

This composition was present at about 10% in the organosilane mixtureused for experimental purposes where R₅ and R₆ were —OCH₃ and R₇ waseither —CH₃ or vinyl.

These compositions are illustrative only as indicated by the patentscited for Packo et al. It is also recognized that not all silanes orcombinations will meet each or all of the criteria set out of above.

The lubricant is preferably chosen to be miscible with the organosilanemixture at ambient temperatures to provide proper control of the flow.Preferred lubricants would include those based on fluids such aspolyolesters. Lubricants based on other fluids might be used. Thoseknown to be miscible with organosilanes include, for example, mineraloils, alkyl benzenes and polyalkylene glycols.

Other fluids as alternatives to the lubricant or in combination with thelubricant may also be used provided that they result in an appropriateviscosity for the mixture and are compatible with contents of the system1. In those other systems where the refrigerant is not a carrier for thelubricant, i.e. systems with separate refrigerant and lubricationcircuits, these other fluids may also be added. The restrictionsoutlined elsewhere herein for high-side injection to a 6 vol % max perminute based on oil capacity also apply. These other fluids include, forexample, drying agents, elastomer and metal conditioners, antioxidants,corrosion and rust inhibitors, antiwear agents, metal deactivators, acidand base neutralizers, detergents, fluorescent and phosphorescent dyesand such. Drying agents include, for example, mono- and polyhydricalcohols, including glycols, preferentially mono-, di- and trihydricalcohols, organosilanes, or so-called orthoformates. Conditionersinclude, for example, methylene chloride and cyclohexanone. Antioxidantsinclude those based on phenolic and aminic derivatives. Corrosion andrust inhibitors include, for example, esters of derivatives fromsuccinic acid. Antiwear agents include, for example, sulphur andphosphorus derivatives. Metal deactivators include, for example,triazole derivatives. Acid and base neutralizers include, for example,buffering agents. Detergent additives include, for example, non-ionicdetergents.

Other sealants, alternative to or in combination with organosilanes, mayalso be used. These sealants may consist of polymeric latexes, vinylacetates, acrylonitriles, epoxide or methacrylates or some combinationthereof. The sealant may include alkylene glycol. The sealant maycontain a catalyst or accelerator. The catalyst may contain a copper orcobalt compound. The catalyst or accelerator may contain a solubilizer.The sealant may contain a filler. The filler may be graphite, carbonpowder or a polytetrafluoroethylene.

Preferred compositions of the lubricant/organosilane mixture are thoseproviding viscosities above a viscosity of 7 cst. when measured at 40°C. The choice of this viscosity minimum was determined by experiment asillustrated below in examples 4 to 7. The 40° C. measurement point isused simply because this is the temperature at which compressorlubricants are typically characterized for viscosity.

The quantity of organosilane to be added depends on the size of therefrigeration or air conditioning system. This is not due to the size ornumber leaks in the system. For small leaks, say less than 1/16 ″ indiameter, and a sealant plug 1/16 ″ long, several hundred seals wouldeasily require only an ounce of organosilane. The rapidity with which aleak will seal depends on delivering an effective quantity of thesealant to the situs of the leak. This latter consideration, experiencein automotive applications, and general practical considerations such asthe size of the injection apparatus, suggest that injections of between⅛ and 1 oz. of organosilanes are sufficient for most applications, withlarger systems requiring the larger amount. In addition, it has beenfound that injections up to a maximum of 10% of the lubricant quantityin the system are recommended due to concerns with injection of liquidinto the low side in proximity to the compressor.

In the preferred embodiment, organosilane is combined with a misciblelubricant. The quantity of lubricant mixed with the organosilane isdetermined by considerations of first, providing adequate lubrication asthe fluid enters the compressor as has been previously described andsecond, of producing limited effect on the final lubricant viscosity,preferably no more than 10% reduction, once the organosilane has beendistributed throughout the system.

The desired viscosity of the lubricant/organosilane mixture can beachieved by varying the ratio of the two or by adjusting the viscosityof the lubricant. Organosilanes of interest generally have very lowviscosities (<1 cst. @ 40 C) while lubricants of interest are muchhigher in viscosity.

(10 to 220 cst. or more @ 40 C). The effect of the injected mixture onthe final lubricant mixture depends on the injected viscosity as well asboth the viscosity and quantity of oil in the system. Table 2 providesinformation on the range of characteristics of typical refrigeration andair conditioning systems. As described previously, the systems in Table2 cover the range of compressor drives and types. The methods andconsiderations outlined in herein apply to all such systems. TABLE 2CHARACTERISTICS OF TYPICAL REFRIGERATION AND AIR CONDITIONING SYSTEMSOIL VISCOSITY SYSTEM SUMP RECOMMEN- CAPACITY TYPICAL CAPACITY DATION(TON/HR.)* APPLICATION (OZ.) (CST. @ 40° C.) 300- Residential 10-3010-32 18,000 BTU/hr Commercial refrigeration, air conditioning 18,000-Residential 30-65 32, 46 60,000 BTU/hr Commercial refrigeration, airconditioning 60,000 BTU/hr Commercial, 65-512 32, 46, 68 (5 ton) - 25industrial refrigeration an air conditioning 25+ Industrial 65-900 46,68 up to 220 applications and greater*1 ton represents approximately 12,000 BTU

Given the wide range of possibilities represented in Table 2, it wasfound to be convenient to evaluate the effect of various injectedlubricant viscosities, lubricant/organosilane ratios, oil sump size andoil sump viscosity by calculation of these factors. This process guidesselection of the preferred viscosity and quantity of the injectedmixture. The following serves to illustrate the process only.

The viscosity of a binary mixture of similar materials is often relatedto the viscosity of the components by the relation:lnη _(mix) =x ₁ .lnη ₁ +x ₂ .lnη₂ +C  (Equation 1)where:

-   -   ln is the natural logarithm    -   η_(mix) is the viscosity of the mixture    -   η₁, η₂ are the viscosities of components 1 and 2 and    -   x₁ and x₂ are the corresponding mole fractions    -   C is a constant dependent on the nature of the components.

This equation has been found to predict the viscosity oforganosilane/lubricant mixtures quite well for the current application.A similar relationship can be written for multicomponent mixtures aswell as for calculation of densities.

With component 1 taken as the injected material and component 2 as theoriginal sump oil, Equation 1 can be rearranged to give the finalviscosity of the mixture as:η_(final)=exp(x _(inj) .ln η _(inj) +x _(sump) .lnη _(sump)+C)  (Equation 2)where

-   η_(final) is the final viscosity of the sump mixture after injection    of the sealant mixture-   ln is the natural logarithm and exp is the exponential-   x_(inj), is the mole fraction of injected material in the final sump    mixture-   x_(sump) is the mole fraction of the original sump oil in the final    sump mixture-   η_(inj), η_(sump) are the viscosities of the injected material and    original sump oil respectively-   C is a constant dependent on the nature of the components.

With the limit that the final sump viscosity should not be lowered morethan 10% compared to the original sump viscosity, then based on Equation2, this amounts to a requirement that:exp(x _(inj) .lnη _(inj) +x _(sump) .lnη _(sump) +C)≧0.9η_(sump)  (Equation 3)Since the mole fraction of any component depends on the weight percentpresent for that component, then Equation 3 provides a basis fordetermining the desired viscosity and quantity limits on the injectedmaterial.

Of course, Equation 3 can be adjusted based on any selected limit onfinal viscosity other than the 90% of original sump viscosity used here.exp(x _(inj) .lnη _(inj) +x _(sump) .lnη _(sump) +C)≧Fr.η_(sump)  (Equation 4)where Fr is the desired fraction of the original sump oil viscosity tobe maintained.

Examples of these predicted effects using Equation 2 are shown forvarious situations in Table 3. TABLE 3 VISCOSITY EFFECTS OFLUBRICANT/ORGANOSILANE MIXTURES ON REFRIGERATION SYSTEMS 1 2 8 LubricantLubricant 3 5 Final Oil Viscosity Viscosity System 4 Viscosity of 6 7Sump in system injected Oil Volume Lube/Organosilane Weight % Weight %Viscosity (cst. @ 40° (cst. @ 40° Capacity Injected Injected LubricantOrganosilane (cst. @ 40° C.) C.) (oz.) (oz.) (cst. @ 40° C.) InjectedInjected C.) 1 32 — 10 1 0.6 0 100 18.7 2 10 32 10 1 10 76 24 9.9 3 3232 10 1 15.6 87.5 12.5 29.9 4 32 32 30 1 10 79 21 30.7 5 32 32 30 1 7 7129 30.2 8 32 32 50 1 10 79 21 31.2 9 32 32 50 2 10 79 21 30.4 10  32 3250 3 10 79 21 29.7 11  46 32 65 3 10 79 21 42.2 12  68 32 512  3 10 7921 66.9

As seen in row 1 of Table 3, the injection of 1 oz. of these particularorganosilanes causes a drop in viscosity in a 10 oz. sump from 32 tobelow 19 cst. (all viscosities will refer to 40 C). A maximum drop insump viscosity of about 10% is generally acceptable, corresponding to 29cst. limit for units designed for 32 cst. viscosity oils. In such smallsystems, our testing indicates that this low viscosity material wouldcause bearing seizure. Rows 2 and 3 of Table 3 show that injection oforganosilane blends with a 32 viscosity lubricant can providesatisfactory results. In row 2, it is indicated that 1 ounce of amixture containing about ¼ ounce of an organosilane mixture and ¾ ounceof a POE lubricant having a viscosity of 32 cst. at 40 C combine to forma mixed viscosity of 10 cst. When this is injected into a systemcontaining 10 ounces of a lubricant having a viscosity of 10 cst. at 40C, the resultant sump viscosity of the mixture is expected to be justbelow 10 cst., at about 9.9 cst. at 40 C. This result is due to theeffect of the molar fraction term in equation 1. Line 3 similarly showsthat injecting ⅛ of an ounce of organosilane in 1 ounce of thelubricant/organosilane mix into such a system using a 32 cst. lubricantrather than a 10 cst. would produce a sump viscosity of 29.9 cst. Thisis above the suggested 29 cst. limit for this lubricant and would be anacceptable formulation. Rows 4 and 5 show information for systems usinga 32 cst. lubricant and having a sump capacity of 30 ounces. Up to about⅕ of an ounce of organosilane can be injected while still maintaining aninjected viscosity of at least 7 cst. Rows 8, 9, and 10 indicate thediminishing effect of larger sump size with various injections comparedto the previous rows, allowing up to ⅗ of an ounce of organosilane to beinjected while still maintaining final viscosity above 29 cst. Rows 11and 12 give information for systems using 46 or 68 cst. lubricants inthe sump.

An example of the use of this computational technique is thedetermination of the best combination of lubricant and organosilane tobe injected by consideration of the system characteristics exhibited inTable 2. For example if a small unit with a 10 oz. sump contains 32 cst.lubricant, what should be the composition of the injected material usinga 32 cst. lubricant and an organosilane mix? With 1 ounce injected, themaximum amount of organosilanes used here is calculated to be 0.175 ofan ounce with the injected mixture having a viscosity of 12 cst. and thesystem lubricant having a final viscosity of 29 cst. At the minimuminjected viscosity of 7 cst., then 0.6 ounces of a mixture containing28.7% organosilanes could be added to the 29 cst. final viscosity,representing 0.172 ounces which is slightly lower.

Table 4 gives examples of situations where the viscosity limit oflubricant (32 cst)/organosilane mix needs to be controlled above theminimum viscosity requirement of 7 cst. dependent on the total amountinjected. For example, to maintain a 10 oz. system containing 32 cst.lubricant above 29 cst. after addition of 1 oz. of mixture, then thelubricant/organosilane mixture should be at a minimum viscosity of 12cst. at 40 C which correspond to less than 0.175 oz. of organosilane inthe 1 oz. of material injected. In the case of injecting 3 ounces ofthis lubricant/organosilane mix into a system containing 30 oz. of 32cst. lubricant, then a similar minimum viscosity holds. The minimumviscosity for a larger system with 65 oz. of 46 cst. oil is limited to amaximum of 0.81 oz organosilanes when the total charge is 3 oz. in orderto keep final viscosity above 41.4 cst. With the 65 oz. sump size, aunit using 68 cst. oil would be limited to a minimum viscosity injectedof 17 cst. corresponding to just over ½ oz of silane in a 3 oz. totalcharge to maintain final viscosity above 61.2 cst. Dropping the injectedcharge to 2 oz. actually yields little benefit in organosilane injectedin this case and also has a much lower injected viscosity for theinjected material at the minimum injected viscosity. TABLE 4 DEPENDENCYOF INJECTED VISCOSITY ON REFRIGERATION AND AIR CONDITIONING SYSTEMSMinimum Sump Lubricant Injected Viscosity Maximum size Grade AmountInjected** organosilane (oz.) in Sump (oz)* (cst. at 40° C.) injected(oz) 10 32 1 12 0.175 30 32 3 12 0.525 65 46 3 8.2 0.81 65 68 3 17 0.5165 68 2 7.6 0.6*lubricant of 32 cst. at 40° C. combined with organosilanes**to 90% viscosity limit in sump viscosity.

It is not required that the viscosity of the injected lubricant be thesame as the lubricating oils in the system, only that there be effectiveinjection of the sealant and non-deleterious longer term effects. Theeffect of increasing the viscosity of the injected mixture using higherlubricant viscosity, however, is relatively small as seen in Table 5which shows the effect of introducing an organosilane/POE lubricant mixinto a unit designed to operate with a lubricant at 32 cst. TABLE 5EFFECT OF VARYING LUBRICANT VISCOSITY OF INJECTED ORGANOSILANE MIXTUREINTO SYSTEM USING 32 CST. POE LUBRICANT * Injected Wt. % Viscosity FinalSystem Viscosity Wt. % Organo- Injected Viscosity (cst @ 40° C.) POEsilane (cst @ 40° C.) (cst. @ 40° C.) 1 32 79 21 10 28.5 2 46 79 21 1329.0 3 68 79 21 17 29.6* 10 oz. sump capacity, 1 oz. injected.

The application of Equations 1-4 allows calculation of the mostdesirable mixture of lubricant and organosilane to be used for anyspecific situation in terms of the size of the unit (oil capacity) andviscosity of the sump oil. The minimum ratio of lubricant toorganosilane is predetermined by the minimum allowable injectedviscosity and the individual viscosities of the lubricant andorganosilane in the injected mixture. The viscosity of mixtures relateexponentially to component viscosities and in ratios dependent on molefractions rather than simple weight fractions. In addition, it isrecognized that the molecular nature of the lubricant affects therelation between viscosity and molecular weight so that the examplespresented here are not to be taken as representing the only possibletrends.

These examples demonstrate that the application of the techniquesdescribed herein is not limited to fluids of a particular viscosityexcept as related to effective injection and longer term operation ofthe system particularly as related to the compressor.

Some systems operate with a lubricating subsystem that is independent ofthe refrigerant. In this case, organosilanes alone are injected into therefrigerant circuit.

It is also possible to inject organosilanes alone in systems where thelubricant is carried by a miscible refrigerant. In this case, theorganosilane alone, or in a mix with lubricant, can be injected into thehigh side of a refrigeration system while the unit is operating up to amaximum of 6% per minute of the systems total oil content. For example,a system with a 50 oz oil capacity could be injected up to a rate of 3oz/min. of organosilanes. The quantity injected remains limited by theforegoing based on limits to reduction in sump viscosity. After 6% isexceeded, there will be a decreased level of compressor performance dueto higher discharge temperature resulting in possible decreased oilreturn to the low side of compressor eventually damaging the shaftbearings. Injecting at a rate above 8% per minute of the total oilsystem's content will likely result in loss of effective heat transfer,decreased bearing lubrication and possible catastrophic compressorfailure. It is recognized that the 6% and 8% amounts are for typicalsystems and there are likely systems that can exceed these thresholdswhile falling within the principles described herein.

The sealant could also be injected into the high side of the unit whileit is out of service and in a vacuum state with all refrigerantsremoved. Once injected into the high side, the system is recharged usingrefrigerant gas or liquid into the high-side up to at least 60% of thesystems full charge. This is carried out while the unit is turned off.The system is then allowed to completely equilize before turning theunit on and topping off the required system's charge.

These methods can be utilized regardless of the class of compressor.

In the preferred embodiment, injection of the lubricant/organosilanemixture is accomplished through the use of a sealed canister 15 and acoupling hose assembly 16 that is first fitted to the canister 15 andthen to the inactive refrigeration system 1 through an injection port 17on the low-pressure side of the compressor 5.

The canister 15 can be pressurized before the canister 15 is sealed. Thepressure in the canister 15 causes the sealant mixture to enter thesystem 1 when the canister is opened, there is fluid connection to thesystem 1, and the system 1 is running to cause “low side” 10 pressuresto drop. In test environment the canister 15 was not pre-pressurized aswill be explained below; however, a charged pressure of 100 psig wasfound to be acceptable for allowing the sealant mixture to enter thesystem 1 in the test environment, where the low side pressure was 77psig as mentioned previously.

Alternatively, the sealed canister 15 can have a pressure near, at orbelow ambient. The canister 15 can be charged (pressurized) using thesystem 1 pressure. First the system 1 is turned off and pressure withinthe system 1 is allowed to equalize. In the test environment, thisresults in an overall system 1 pressure of approximately 100 psig. Thecanister 15 is then placed in fluid connection with the system 1. Thiscauses the canister 15 to be pressurized to approximately 100 psig. Thesystem 1 can then be run. This causes the pressure in the low side 10 todrop. The higher pressure within the canister 15 causes the sealantmixture to enter the system 1.

Using a non-pressurized canister 15 as described above is preferred assuch containers are less hazardous. This means, for example, that theyare transportable without having to comply with the stricttransportation regulations applicable to pressurized containers.

More details of a preferred method used in the test environment will nowbe described. Before use, the canister 15 is at a pressure of about 20inches of mercury vacuum. The vacuum is a result of packaging processesthat ensure much of the air is removed from the canister 15 before it issealed. Hose assembly 16 is evacuated and then the canister 15 seal isbroken using a can-tapper 21 that is built into the hose assembly 16 insuch a way that refrigerant mix from the system 1 is allowed into thecanister 15 until pressures are stabilized, and the canister 15 ischarged. The can-tapper 21 has a manually operated valve (see valvehandle 25 below) for fluid connection (open) and fluid disconnection(closed) of the canister 15 from the system 1. It also has a tapping pin(operation described below) for unsealing the canister 15 (which is alsorequired for fluid connection when the canister 15 is sealed). Thecan-tapper 21 is also a fitting for sealed fluid connection to thecanister 15, typically by way of compatible threads in the can-tapperand on the canister 15, and corresponding seals, such as a rubber gasketor an o-ring.

The addition of canister 15 contents to the refrigerant system 1 iscontrolled to a maximum flow rate of about 6 cc/sec which in thepreferred embodiment is obtained through the use of orifice 20 having amaximum diameter of about 0.06 in. One such arrangement is shown in FIG.2. Although there is no minimum flow rate required, the minimum orificesize should be about 0.02 inches in diameter to avoid orifice pluggingdue to contamination from particles from system 1 as the canister 15 ischarged. This minimum restriction could be removed by the inclusion of afilter in the injection hose between the fitting 22 and the injectionport 17 shown in FIG. 2.

The orifice 20 is located within fitting 22 of FIG. 2. In the testenvironment an orifice of 0.0292 inches diameter was successful. Thehose assembly 16 has a hose 23 between the can-tapper 21 and the fitting22.

Surprisingly, it has been found that the action of filling the canister15 with refrigerant upon tapping the canister 15 and opening a valve inthe tapper 21 causes the canister 15 and its contents to heat totemperatures well above ambient. Temperatures of 135° F. wereencountered in tests. This may affect the flow rate of the organosilaneas it enters the system 1. In the preferred embodiment, the canister 15is fluidly disconnected after charging and the system 1 is run. Then thecanister 15 is again fluidly connected to the system 1. This allows thesystem 1 to achieve full low side 10 pressure that will best allow thesealant mixture to enter the system 1.

As there is a period of time between disconnecting and re-connecting thecanister 15, the canister 15 should be allowed to cool to at or nearambient temperature while still fluidly connected to the non-runningsystem 1. If not, then charge in the canister 15 may be lost as pressurewill drop with the temperature in a closed canister 15.

Also, the contents of the canister 15 should enter the cooler suctiongas stream with as close to ambient temperature of the system 1 aspossible so as not to effect the volume of the cooler gas going to thecompressor 5. A compressor 5 generally requires at least a four percentreturn of oil to maintain adequate lubrication on metal-to-metalsurfaces. In practical terms, a residential system 1 operating at asuction pressure of 70 psig will typically have a correspondingevaporator 3 saturation temperature of 41 degrees F. If the system 1 isoperating satisfactorily then the actual suction line 10 temperatureshould be approximately 51 degrees F. This is due to an extra 10 degreesof superheat picked up during the expansion. Elevating this temperaturemomentarily could cause an erratic expansion of gas followed bycontraction resulting in a cavitation effect on the compressor 5.Experiments show a fluctuation in low-side and high-side pressures whenthe product has not been sufficiently cooled. Rapid changes of pressurecan damage compressor valves and discharge excess oil from thecompressor sump into the high-side line. This excess oil will begin tolog and affect downstream conditions such as temporary high dischargepressures accompanied by temporary low-side pressure. The percentage ofrequired oil to be carried back could lower to the point of notsupplying adequate lubrication to metal-to-metal contact causing damageto the compressor 5.

These and other steps in the procedure of the preferred embodiment aredescribed in Table 1. TABLE 1  1. Turn off A/C system 1 and allow enoughtime for refrigerant to equalize in system 1.  2. Confirm thatcan-tapper 21 piercing pin is fully retracted below seating washer.(Turn valve handle 25 counter-clockwise, opening the valve in the tapper21)  3. Thread canister 15 onto can-tapper 21 by turning clockwise. Becareful not to cross thread or over tighten.  4. Thread female fitting22 onto vacuum pump, not shown, and draw vacuum for approximately 1minute to eliminate air in tap hose 5.  5. Remove female fitting 22 fromvacuum pump while it is running to maintain vacuum in tap hose 5. Afterdisconnecting shut down vacuum pump.  6. Thread female fitting 22 ontolow side service port 17 immediately after removing from vacuum pump. 7. Turn can-tapper 21 piercing handle 25 clockwise until it stops.(This action pierces the can, and closes the valve in the can-tapper21.)  8. Hold canister 15 upside down and above the low side serviceport 17. Turn handle 25 counter-clockwise (open the can-tapper valve andprovided fluid connection between the canister 15 and the system 1)slowly allowing the system 1 refrigerant to fully charge canister 15.The canister 15 will become warm once the refrigerant mixes with itscontents. Allow the canister 15 to dissipate the additional heat ofcharging which should take between 5 to 10 minutes depending on system 1charge and ambient air conditions. When the can's temper- ature hasequalized with ambient air conditions then proceed with next step. Besure to check that all connections from canister 15 to system 1 aresecure and that there is no leakage occurring. The primary reason forinverting the canister is to simplify the procedure for the technician.If the technician forgets to invert the canister before injection intothe air-conditioning unit (see 10. below) then the transfer of themixture would not be successful because of the gas on top and theheavier liquid residing on the bottom of the can. The connection to thelow-side charging port is made with the canister inverted for chargingand injection as one-step. This also limits stressing the hose assemblyby changing position while under pressure. Having the gas first passthrough the mixture also helps to mix the contents of the mixture ifpossible stratification occurred between the organosilane and themiscible lubricant.  9. Turn handle 25 clockwise until it stops,isolating charged canister 15 from A/C or R system 1. 10. While holdingthe canister 15 upside down turn on A/C system 1. Slowly turn handle 25counter-clockwise gradually releasing sealant into the system 1. Thisshould take approximately 3 to 5 minutes. Releasing sealant too quicklycould result in liquid slugging. Shake canister 15 gently to determinewhen empty. If all of the contents in canister 15 are not emptied after5 minutes then turn canister 15 tapper 21 piercing handle 25 clockwiseuntil it stops. Turn of A/C or R system 1 and repeat steps 8, 9 and 10.11. Once canister 15 is empty remove female fitting 22 from low sideservice port 17, then shut down A/C system 1. Allow system 1 pressure toequalize. The A/C or R system 1 should be left off for approx. 5minutes. This procedure allows product to mix with systems 1 oil andwhen the system 1 is restarted will allow for equal distributionthroughout system 1.

In typical experiments performed during the course of the currentdevelopment, a canister was used with approximate dimensions of 5 cm.diameter and 10 cm height and this contained about 89 cc (3 oz.) of alubricant/organosilane mix. With the canister 15 filled with refrigerantand inverted at ambient conditions, this would produce a lower column ofliquid about 4.5 cm. high covered with a gaseous column of refrigerant5.5 cm. in height. The pressure exerted by the refrigerant was around120 psi and this was then injected into a system operating at 66 psi.Thus the driving force for injection of the liquid phase into the systemwas about 54 psi.

In an ideal situation the equationQ=C _(d) ×A×(2×ΔP/ρ) ^(1/2)  (Equation 5)could be applied where

-   Q is flow rate-   C_(d) is the coefficient of discharge-   ΔP is the differential pressure, and-   ρ is the fluid density.

Experiments in transparent glass vessels showed the expected result thatthe liquid actually contained bubbles of refrigerant. Nevertheless,considering the ideal one-phase flow situation, equation 5 can beapplied to obtain at least a model of the injection process. For anorifice of 0.029 inches in diameter, the canister was found to empty inabout 90 sec. This corresponds to a coefficient of discharge of 0.37.Experiments showed that satisfactory injections could be made usingorifice sizes up to about 0.060 inches. This corresponds to an initialflow rate of 6 cc/sec and a final flow rate of 4 cc/sec for the lastfraction of the liquid.

Considerations of system size relate to the effect on viscosity of thelubricant in the system which tends to increase with the size of thesystem itself. System size is typically measured in tons—a measure ifthe cooling capacity of the system 1 (1 ton is equivalent to thedelivery of 12,000 BTU cooling capacity per hour). General considerationof these factors provide “rules of thumb” to guide quantities oforganosilane mixture to be added. For example, one scenario suggests forunits above 5 tons capacity, a mixture about 7-8 cst. @ 40 C isappropriate and about 10 cst. for smaller units. The actual totalquantity of lubricant/silane mix is dependent on ensuring effectivedelivery of sealant material to the situs of the leak. Typically, unitsbelow 1 ton should require about ⅛-¼ oz. of organosilane and largerunits ½-1 oz. The total quantities of the mixture will also depend onthe practicality of the details of the injection system being used. Theviscosity of the mixture and the quantity of organosilane can beadjusted within these general guidelines.

EXAMPLES

The principles described herein are further illustrated in the followingexamples, but the scope is not limited by these examples.

Test Methods

The general test apparatus is shown schematically in FIG. 2 andrepresents the basic components of a typical refrigeration system 1. Arefrigerant gas (R-22 was used in the test environment; however, R134aand other refrigerants could also be used) is circulated by means of ahermetically sealed electric motor and compressor 5. The gas is cooledto liquid by means of a condenser 7; the liquid passes through anorifice 20 and then through an evaporator 3 where the liquid isregenerated to a gas accompanied by the desired cooling effect. The gasthen returns to the compressor 5 for repeating cycles of the process.

Sealant and mixtures were added by the procedure represented in Table 1to the low pressure (suction) side of the compressor 5.

Sealant

In the base case, simple injection of the organosilane sealant in thelow side port 17 was shown not to be appropriate for hermetically sealedrefrigerant compressor 5 systems 1.

Example 1

In a laboratory test, a 2 ton vertical hermetic single phaserefrigeration system 1 with a full refrigerant load was loaded tosimulate an ambient temperature above 32° C. An organosilane mixture wasinjected into the circuit and the compressor 5 failed after only onefurther hour of operation due to bearing seizure.

Example 2

In another set of tests, two 2 ton single phase piston type systems 1were injected with a mixture of commercial organosilane and immisciblelubricating oil. Failure occurred in one system 1 after 10 minutes andafter 1 hour in the second case.

Example 3

Two small 10,000 BTU packaged refrigerant systems 1 were tested. Bothfailed within 10 hours. Subsequent examination of these systems 1 showedthat failure was due to lack of oil to the upper sleeve bearing,referred to as the compressor 5 outboard bearing.

Sealant Viscosity

The effect of sealant viscosity was investigated by varying the ratiosof organosilane and lubricating oil in the sealant mixture.

Example 4

Mixtures of organosilane sealant (viscosity<1 cst@ 40° C.) andimmiscible compressor 5 oil (viscosity 68 cst. @ 40° C.) caused bearingseizure in all five cases in Examples 1,2, and 3.

Example 5

Use of straight organosilane mixture caused compressor 5 bearing seizurewithin one hour in a test with the 2 ton system 1.

Example 6

A test was performed using a 0.029 in. orifice 20 to inject a 3 fl. oz.mixture consisting of 3 parts of a commercial polyolester refrigerationcompressor 5 oil and 1 part of an organosilane sealant such that themixture had a viscosity of 8 cst. @ 40° C. The oil capacity of thesingle phase hermetically sealed 2 ton system 1 was 55 oz. The system 1was injected with the organosilane/oil mixture with no change inamperage of the motor, indicating no liquid slugging. The system 1 wasrun successfully for 12 days until shut down deliberately.

Example 7

A test was performed similar to that described in Example 6 except thatthe mixture injected consisted of 2 parts of the commercial polyolesterrefrigeration compressor 5 oil and 1 part of the organosilane sealant togive a mixture viscosity of 11 cst. @ 40° C.

A start/stop test was run with 60 start/stops over a 3½ hr. period. Thisis a severe test due to the surge of electricity required to start thespinning of the rotor of the motor and also due to some initial loss ofoil from the inboard bearing at each start. The test was successful withno change in operating variables and the system 1 ran for an additional13 days with excellent operation until it was deliberately shut down.

Rate of Injection

Controlled rate of introduction of the organosilane/oil mix wasinvestigated as a variable. The fitting 22 shown in FIG. 1 was used tointroduce mixtures into a 2 ton refrigeration system 1 fitted with anoversized 2½ ton condenser 7. The fitting 22 at one end of the hoseseals and punctures a canister 15 containing the sealant. The fitting 22at the other end is attached to the refrigeration system 1 and a valve 9is opened to allow the sealant mixture to enter the refrigeration system1 through an orifice 20. The size of this orifice 20 affects theinjection rate of the sealant.

Example 8

Using an orifice 20 size of 0.094 in., it was found that the rate ofaddition of the sealant/oil mixture caused fluctuations in suction anddischarge pressure of the system 1. As previously mentioned this upsetcondition can cause the compressor to momentarily discharge from thesump into the discharge line causing logging possibly affecting oilreturn to the suction side of the compressor and eventual bearingfailure. The needle valve 9 associated with the orifice 20 would notallow sufficient additional fine control to overcome this problem.

Example 9

A capillary tube was used to control introduction of the sealant. Anorifice 20 size of 0.055 in. was found to allow successful introductionof the sealant into the above refrigeration system 1. The system 1 ranfor 18 days with no change in operating variables before it wasdeliberately shut down.

Example 10

Inserting an orifice 20 size of 0.029 in. into the system 1 described inExample 8 was tested and found to give successful injection oforganosilane/oil mixes.

Quantity of Injection

Smaller systems are of the greatest concern for susceptibility to therate and quantity of injection.

The two examples below were injected with a mixture consisting of ¾ ozof polyolester lubricating oil and ¼ oz of a silane mixture having atotal viscosity of 9.8 cst. at 40 C using the injection techniqueoutlined in Table 1. In each case, the sump originally contained 10 oz.of polyalkylene glycol lubricant having a viscosity of 32 cst. at 40 C.Examples 11 and 12 below support an injection limit of up to 10 vol % ofsealant mixture, bases on sump oil charge, can be injected intorefrigeration or air conditioning systems. In addition, it is apparentin these examples that the refrigerant charges are extremely small (3.70and 1.69 oz) but that the additional 10 vol % liquid has had no effecton the thermal efficiencies of the units.

Example 11

DANBY Model DCR433W

-   Refrigerant—134 A-   Charge—105 g-   AMPS—1.1

Procedure: Bullet piercing valve installed

-   Conditions: Base of compressor—101 F to 104 F 0.87 AMPS-   Suction temp—72 F-   Discharge temp—101 F-   Inside panel—freezer 0 to 2 F (Temperature glide effect)-   Allow 3 min to fill can-   5 min cool down-   Allow 5 min run then switch to off-   After stop time, put in operation

After 90 days, the system continued to run successfully.

Example 12

Unit: GE with Matsushita SB30C50GAU6 compressor

-   Refrigerant 134 A-   Charge 1.59 ounces-   Procedure: Bullet piercing valve installed-   Conditions: Base of compressor—90 F 0.88 AMPS-   Suction temp—70 F-   Discharge temp—102 F-   Inside-panel-freezer—4 F to 5 F

Allow 3 min to fill

-   5 min cool down-   Allow 5 min run then switch off-   After stop time, put in operation

After 90 days, the system continued to run successfully

Injection Procedures

As outlined in Table 1, the typical procedure used to inject mixturesinto the refrigeration system 1 involves opening the canister 15containing the oil/organosilane mixture to a low pressure port 17 justprior to the non-operating compressor 5. The mixture is at a pressurenear 20 inches of mercury vacuum before opening to the refrigerantsystem 1 which is typically near 100 psig. The entry of the refrigerantinto the mixture in the canister 15 causes a heating effect and raisesthe canister 15 and contents to about 25° C. above ambient. Single phasesystems 1 are particularly susceptible to this effect since entry of thehot mixture into the refrigeration system 1 would cause momentaryheating of the suction vapor and a decrease in the vapor's density. Thisin turn affects the ability of the vapor to cool the motor and othermechanical parts.

Therefore as part of the procedure to inject the mixture from thecanister 15, it is important to allow the refrigerant/sealant mixture tocool before introduction into the refrigeration system 1.

Variations and modifications can be made without departing from thespirit of this invention. It should be understood that the form of theinvention described above, including the Figures and Tables, isillustrative only and is not intended to limit the scope of the presentinvention.

It will be understood by those skilled in the art that this descriptionis made with reference to the preferred embodiment and that it ispossible to make other embodiments employing the principles of theinvention which fall within its spirit and scope as defined by thefollowing claims.

1. A method for injecting sealant into an air conditioning orrefrigeration system having a compressor, a high pressure side (“highside”), and a low pressure side (“low-side”), the method comprising: a)injecting the sealant in a quantity to provide sufficient lubrication tomaintain proper operation of the compressor when the sealant is fullydistributed in the system, and b) injecting the sealant so as tomaintain proper operation of the compressor before the sealant is fullydistributed in the system.
 2. The method of claim 1, wherein the sealantis injected at the high side of the system so as to maintain properoperation of the compressor before the sealant is fully distributed bydistributing the sealant starting at the high side.
 3. The method ofclaim 1, wherein the sealant is injected at a controlled rate so as tomaintain proper operation of the compressor before the sealant is fullydistributed in the system.
 4. The method of claim 1, wherein the sealantis injected into a non-operating system under vacuum, and other systemcontents, including refrigerant, are later injected into the systemcausing distribution of the previously injected sealant.
 5. The methodof claim 1, sealant is injected as a part of a fluid mixture, and themixture further comprises one or more of lubricant, drying agent,corrosion/rust inhibitor, antiwear agent, fluorescent or phosphorescentdye.
 6. The method of claim 1, wherein the sealant is an organosilane.7. The method of claim 6, wherein the organosilane is a monomer capableof forming a solid polymer with itself or other chosen organosilanes inthe presence of moisture, and is stable in the absence of moisture, anddoes not substantially interfere with the normal operation of othercontents of the system in selected quantities.
 8. The method of claim 2,wherein the injected sealant is injected at a rate of less than 6% perminute of lubricant within the system.
 9. The method of claim 4, whereinapproximately 60% of total system refrigerant injected after thesealant.
 10. The method of claim 1 wherein the sealant is part of afluid mixture further comprising a lubricant.
 11. The method of claim 10wherein the lubricant is an oil, the compressor has a sump containingoil, and the minimum viscosity of the injected fluid mixture is Tinj asdetermined by:exp(x _(inj) .lnη _(inj) +x _(sump) .ln η _(sump) +C)≧Fr.η _(sump)where, ln is the natural logarithm and exp is the exponential, x_(inj),is mole fraction of injected material in final sump mixture, x_(sump) ismole fraction of original sump oil in final sump mixture, η_(inj),η_(sump) are viscosities of the injected material and original sump oilrespectively, and Fr is a desired fraction of original sump oilviscosity to be maintained.
 12. The method of claim 11 wherein Fr=0.9.13. The method of claim 10, wherein the viscosity of the mixture is notless than 7 CST @ 40° C.
 14. A method of introducing sealant into an airconditioning or refrigeration system having a compressor and evaporator,the method comprising the steps of: a) connecting a vessel containing asealant mixture comprising an organosilane between the compressor andthe evaporator, and b) while the system is running, allowing the sealantmixture to enter the system at a rate to prevent liquid slugging and tomaintain sufficient concentrations of lubricant for proper operation ofthe compressor during the injection process, c) allowing the sealant toenter the system in an amount to maintain sufficient compressorlubricant viscosity for continued proper operation of the compressor d)allowing the sealant to enter in an amount that will allow continuedproper operation of the air conditioning or refrigeration system. 15.The device and method of claim 1 where the sealant may be one or more ofan organosilane and a polymeric latex consisting of one or more of avinyl acetate, methacrylate, nitrile, epoxide and styrene polymer. 16.The method of claim 1, wherein the mixture further comprises one or moreof an accelerant and a catalyst.
 17. The method of claim 14, whereinallowing the sealant mixture to enter the system comprises pressurizingthe sealant mixture sufficiently above system low side operatingpressure to cause the sealant mixture to enter the system from thevessel when the system is running.
 18. The method of claim 17, whereinpressurizing the sealant mixture comprises using the system pressure ofthe system in a non-running state to pressurize the sealant mixture inthe vessel.
 19. The method of claim 18 further comprising a step ofallowing the sealant mixture to cool to near ambient temperature afterthe vessel is pressurized and while the vessel is fluidly connected tothe system in the non-running state.
 20. The method of claim 19, furthercomprising the step of fluidly disconnecting the pressurized vessel fromthe system after cooling, running the system until low side pressuredrops, and fluidly connecting the vessel to the low side of the systemand allowing the sealant to enter the system as provided in step b). 21.A method of introducing sealant into an air conditioning orrefrigeration system having a compressor and an evaporator, the methodcomprising the steps of: a. turning off the system; b. allowing systempressure to equalize; c. connecting a vessel containing a sealantmixture comprising an organosilane between the compressor and theevaporator, and d. while the system is running, allowing the sealantmixture to enter the system at a rate to prevent liquid slugging and tomaintain sufficient concentrations of lubricant for proper operation ofthe compressor wherein, the organosilane is a monomer capable of forminga solid polymer with itself or other chosen organosilanes in thepresence of moisture, and is stable in the absence of moisture in thesystem, and does not substantially interference with the normaloperation of contents of the system in selected quantities.
 22. Themethod of claim 21, wherein the step of connecting the vessel furthercomprises providing fluid connection between the vessel and the system,and the method further comprises allowing sufficient time for thesealant mixture to achieve ambient temperature before running the systemafter fluid connection.
 23. The method of claim 21, further comprisingthe step of: e) turning off the system when a selected amount of sealantmixture has entered the system for a period of time to allow systempressure to equalize, and f) repeating step d) g) repeating steps e) andf) until a total selected amount of sealant has entered the system. 24.The method of claim 9, further comprising equilibrating the system afterinjecting the approximately 60% of the refrigerant then turning on thesystem and adding remaining refrigerant.
 25. The method of claim 21,wherein the sealant mixture has a viscosity above 7 cst. when measuredat 40° C.
 26. The method of claim 25, wherein the maximum flow rate ofinjection is 6 cc/sec
 27. The method of claim 21 wherein the minimumviscosity for a particular lubricant/sealant mixture is η_(inj) asdetermined by:exp(x _(inj) .lnη _(inj) +x _(sump) .lnη _(sump) +C)≧Fr.η _(sump) where,ln is the natural logarithm and exp is the exponential, x_(inj), is molefraction of injected material in final sump mixture, x_(sump) is molefraction of original sump oil in final sump mixture, η_(inj), η_(sump)are viscosities of the injected mixture and original sump oilrespectively, and Fr is a desired fraction of original sump oilviscosity to be maintained.
 28. The method of claim 11 wherein Fr=0.9.29. The method of claim 27 wherein if the calculated viscosity is below7 cst., then the minimum viscosity is 7 cst.
 30. The method of claim 25,wherein step of allowing the sealant to enter the system furthercomprises allowing the sealant to enter through an orifice having anopening within a range of from 0.020-0.06 inches diameter.
 31. Themethod of claim 22, wherein the step of connecting the vessel to thesystem comprises connecting a hose assembly between the vessel and a lowpressure side service port of the system.
 32. The method of claim 23,wherein the hose assembly further comprises a first fitting forconnection to the vessel and a second fitting for connection to theport.
 33. The method of claim 32, wherein the step of providing fluidconnection between the vessel and the system, and the step of allowingsealant mixture to enter the system, comprise opening a valve in thesecond fitting.
 34. The method of claim 33, wherein the vessel is asealed canister, and wherein the step of providing a fluid connectionbetween the canister and the system further comprises tapping thecanister before opening the valve in the second fitting.
 35. The methodof claim 34, wherein the second fitting is a can-tapper.
 36. The methodof claim 31, comprising the step of substantially evacuating the hoseassembly prior to connection to the system.
 37. A device for introducingsealant into a hermetically sealed air conditioning or refrigerationsystem, the device comprising: a. A sealed vessel comprising anorganosilane mixture of an organosilane and a miscible material, themixture having a viscosity above 7 cst. when measured at 40° C. wherein,the organosilane is a monomer or oligomer capable of forming a solidpolymer with itself or other chosen organosilanes in the presence ofmoisture, and is stable in the absence of moisture in the system, anddoes not substantially interference with the normal operation ofcontents of the system in selected quantities.
 38. The device of claim37, further comprising a metering device for fluid connection with thesealed vessel, and for controlling fluid flow from the sealed vessel.39. The device of claim 38, wherein the metering device is an orificehaving an opening within a range of from 0.020-0.06 inches.
 40. Thedevice of claim 39, further comprising a fitting for sealed fluidconnection to a low side port of the system, and wherein fluid flowingthrough the metering device also flows through the fitting.
 41. Thedevice of claim 37, further comprising a hose assembly with a firstfitting for sealed fluid connection to a low side port of the system,and a sealed fluid connection to the sealed vessel.
 42. The device ofclaim 41, further comprising a metering device for controlling fluidflow from the sealed vessel through the hose assembly.
 43. The device ofclaim 42, wherein the fluid connection to the sealed vessel is a secondfitting.
 44. The device of claim 43, wherein the second fittingcomprises a manually operable valve for providing fluid connectionbetween the hose assembly and the sealed vessel.
 45. The device of claim44, wherein the second fitting further comprises a can-tapper foropening the sealed vessel.
 46. The device of claim 45 where a filter isplaced between the fitting connecting to the system and the orifice 47.The device of claim 46 where the orifice has a maximum diameter of 0.06inches.
 48. The device of claim 45, wherein the sealed vessel is asealed canister.
 49. The device of claim 37, wherein the organosilane orcomponents of the organosilane mixture can be represented as(R₁)(R₂)Si(R₃)(R₄) where, R₁=is an alkyl radical of 1-4 carbon atoms orvinyl or —OH R₂ is R₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂, R₃ isR₁ or —OR₁ or —NH(R₁) or —N(R1)₂ or —R₁NHR₁NH₂, and R₄ is R₁ or —OR₁ or—NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂
 50. The device of claim 37 wherein acomponent of the organosilane mixture can be represented as(R₅)(R₆)(R₇)Si—O—Si(R₅)(R₆)(R₇) R₅, R₆ or R₇ are each any one ofR₁,R₂,R₃ or R₄ where, R₁=is an alkyl radical of 1-4 carbon atoms orvinyl or —OH, R₂ is R₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂ R₃ isR₁ or —OR₁ or —NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂ and R₄ is R₁ or —OR₁ or—NH(R₁) or —N(R₁)₂ or —R₁NHR₁NH₂
 51. The device of claim 37, wherein thesealant mixture further comprises a lubricant miscible with theorganosilane and refrigerant for use in the system.
 52. The device ofclaim 50 wherein the miscible mixture comprises a lubricant selectedfrom one or more of a polyol ester, polyalkylene glycol, mineral oil,polyalphaolefin and alkylbenzene.
 53. The device of claim 51 wherein themiscible mixture comprises a lubricant further comprising additives toenhance and refresh the performance of lubricant in the sscompressor.